Rozkov Aleksei, Larsson Bert, Gillström Stefan, Björnestedt Robert, Schmidt Stefan R
Global Protein Science & Supply, DECS, AstraZeneca R&D, Södertälje, S-15185 Sweden.
Biotechnol Bioeng. 2008 Feb 15;99(3):557-66. doi: 10.1002/bit.21603.
Transient expression of recombinant proteins in mammalian cell culture in a 100-L scale requires a large quantity of plasmid that is very labour intensive to achieve with shake flask cultures and commercially available plasmid purification kits. In this paper we describe a process for plasmid production in 100-mg scale. The fermentation is carried out in a 4-L fed-batch culture with a minimal medium. The detection of the end of batch and triggering the exponential (0.1 h(-1)) feed profile was unattended and controlled by Multi-fermenter Control System. A restricted specific growth rate in fed-batch culture increased the specific plasmid yield compared to batch cultures with minimal and rich media. This together with high biomass concentration (68-107 g L(-1) wet weight) achieves high volumetric yields of plasmid (95-277 mg L(-1) depending on the construct). The purification process consisted of alkaline lysis, lysate clarification and ultrafiltration, two-phase extraction with Triton X-114 for endotoxin removal, anion-exchange chromatography as a polishing step, ultrafiltration and sterile filtration. Both fermentation and purification processes were used without optimisation for production of four plasmids yielding from 39 to 163 mg of plasmids with endotoxin content of 2.5 EU mg(-1) or less.
在100升规模的哺乳动物细胞培养中瞬时表达重组蛋白,需要大量质粒,而通过摇瓶培养和市售质粒纯化试剂盒来获得这些质粒非常耗费人力。在本文中,我们描述了一种生产规模为100毫克的质粒制备方法。发酵在4升补料分批培养中使用基本培养基进行。分批培养结束的检测以及触发指数级(0.1 h(-1))补料曲线是无人值守的,并由多发酵罐控制系统控制。与使用基本培养基和丰富培养基的分批培养相比,补料分批培养中受限的比生长速率提高了比质粒产量。这与高生物量浓度(68 - 107克/升湿重)一起实现了高体积质粒产量(95 - 277毫克/升,具体取决于构建体)。纯化过程包括碱裂解、裂解物澄清和超滤、用Triton X - 114进行双相萃取以去除内毒素、阴离子交换色谱作为精制步骤、超滤和无菌过滤。发酵和纯化过程均未进行优化,用于生产四种质粒,产量为39至163毫克,内毒素含量为2.5 EU/毫克或更低。